US2296037A - Cutting oil - Google Patents
Cutting oil Download PDFInfo
- Publication number
- US2296037A US2296037A US2296037DA US2296037A US 2296037 A US2296037 A US 2296037A US 2296037D A US2296037D A US 2296037DA US 2296037 A US2296037 A US 2296037A
- Authority
- US
- United States
- Prior art keywords
- oil
- sulfur
- cutting
- oils
- sulfurized
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000010730 cutting oil Substances 0.000 title description 22
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 42
- 239000011593 sulfur Substances 0.000 description 42
- 229910052717 sulfur Inorganic materials 0.000 description 42
- 238000005520 cutting process Methods 0.000 description 19
- 239000002480 mineral oil Substances 0.000 description 17
- 235000010446 mineral oil Nutrition 0.000 description 16
- 239000010685 fatty oil Substances 0.000 description 14
- 239000003921 oil Substances 0.000 description 13
- 239000000203 mixture Substances 0.000 description 9
- 239000010687 lubricating oil Substances 0.000 description 8
- 239000000463 material Substances 0.000 description 8
- 238000004062 sedimentation Methods 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 4
- 239000010688 mineral lubricating oil Substances 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- YSMRWXYRXBRSND-UHFFFAOYSA-N TOTP Chemical compound CC1=CC=CC=C1OP(=O)(OC=1C(=CC=CC=1)C)OC1=CC=CC=C1C YSMRWXYRXBRSND-UHFFFAOYSA-N 0.000 description 3
- 125000006267 biphenyl group Chemical group 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000003381 stabilizer Substances 0.000 description 3
- 239000010775 animal oil Substances 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000001050 lubricating effect Effects 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- HVLLSGMXQDNUAL-UHFFFAOYSA-N triphenyl phosphite Chemical compound C=1C=CC=CC=1OP(OC=1C=CC=CC=1)OC1=CC=CC=C1 HVLLSGMXQDNUAL-UHFFFAOYSA-N 0.000 description 2
- JYFHYPJRHGVZDY-UHFFFAOYSA-N Dibutyl phosphate Chemical compound CCCCOP(O)(=O)OCCCC JYFHYPJRHGVZDY-UHFFFAOYSA-N 0.000 description 1
- UFWIBTONFRDIAS-UHFFFAOYSA-N Naphthalene Chemical compound C1=CC=CC2=CC=CC=C21 UFWIBTONFRDIAS-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 150000007824 aliphatic compounds Chemical class 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- BVXOPEOQUQWRHQ-UHFFFAOYSA-N dibutyl phosphite Chemical compound CCCCOP([O-])OCCCC BVXOPEOQUQWRHQ-UHFFFAOYSA-N 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 150000008301 phosphite esters Chemical class 0.000 description 1
- OJMIONKXNSYLSR-UHFFFAOYSA-N phosphorous acid Chemical compound OP(O)O OJMIONKXNSYLSR-UHFFFAOYSA-N 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002195 soluble material Substances 0.000 description 1
- 238000005987 sulfurization reaction Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- -1 tricresyl phosphate Chemical class 0.000 description 1
- XZZNDPSIHUTMOC-UHFFFAOYSA-N triphenyl phosphate Chemical compound C=1C=CC=CC=1OP(OC=1C=CC=CC=1)(=O)OC1=CC=CC=C1 XZZNDPSIHUTMOC-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M135/00—Lubricating compositions characterised by the additive being an organic non-macromolecular compound containing sulfur, selenium or tellurium
- C10M135/02—Sulfurised compounds
- C10M135/06—Esters, e.g. fats
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M141/00—Lubricating compositions characterised by the additive being a mixture of two or more compounds covered by more than one of the main groups C10M125/00 - C10M139/00, each of these compounds being essential
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2211/00—Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions
- C10M2211/02—Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions containing carbon, hydrogen and halogen only
- C10M2211/024—Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions containing carbon, hydrogen and halogen only aromatic
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2211/00—Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions
- C10M2211/04—Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions containing carbon, hydrogen, halogen, and oxygen
- C10M2211/044—Acids; Salts or esters thereof
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2219/00—Organic non-macromolecular compounds containing sulfur, selenium or tellurium as ingredients in lubricant compositions
- C10M2219/02—Sulfur-containing compounds obtained by sulfurisation with sulfur or sulfur-containing compounds
- C10M2219/024—Sulfur-containing compounds obtained by sulfurisation with sulfur or sulfur-containing compounds of esters, e.g. fats
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
- C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
- C10M2223/04—Phosphate esters
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2223/00—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions
- C10M2223/02—Organic non-macromolecular compounds containing phosphorus as ingredients in lubricant compositions having no phosphorus-to-carbon bonds
- C10M2223/04—Phosphate esters
- C10M2223/041—Triaryl phosphates
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/20—Metal working
- C10N2040/22—Metal working with essential removal of material, e.g. cutting, grinding or drilling
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2060/00—Chemical after-treatment of the constituents of the lubricating composition
- C10N2060/10—Chemical after-treatment of the constituents of the lubricating composition by sulfur or a compound containing sulfur
Definitions
- This invention relates to sulfurized lubricants, such as cutting oils, and more particularly to light colored or transparent cutting oils of this character.
- Cutting oils as heretofore employed have frequently been composed of fatty or animal oils, and blends of mineral oil with fatty oils. It has also been proposed to sulfurize blends of animal oil and mineral oil, but in such case, the sulfur is taken up ahnost entirely by the more reactive fatty oil to produce a product in which the sulfur is in stable tightly combined form with the fatty oil and diluted by the mineral oil. Cutting oils have also been prepared by incorporating sulfur directly with mineral oil, generally under relatively high temperatures and frequently under superatmospheric pressure to produce a product in which the sulfur is sufiiciently combined with the mineral oil as to resist sulfur separation and sedimentation upon storage.
- the earlier cutting oils consisting of simple fatty oils or blends thereof, as well as the sulfurized blends of mineral oil and fatty oil where the sulfur is taken up ahnost entirely by the fatty oil, do not possess the high cutting efficiency demanded by high speed cutting operations of the present time.
- a satisfactory transparent cutting oil of this character can be produced by sulfurizing a light colored pale mineral lubricating oil under controlled conditions of comparatively low temperature and at atmospheric pressure so as to provide about 1,0435% loosely combined sulfur in the oil, and then enhancing the cutting efiiciency and at the same time stabilizing th sulfurized oil by the addition of a small proportion of certain oil soluble materials of the character of extreme pressure bases, such as tricresyl phosphate.
- a mineral lubricating oil or lubricating oil blend containing light colored pale lubricating oils having a Saybolt Universal viscosity at 100 F. of about 100-l80 seconds, is sulfurized by heating with free sulfur in the absence of added fatty oil or other constituents highly reactive with sulfur at a temperature of about 300-340" F. and preferably about 320 F. for a controlled period of time.
- the quantity of sulfur employed is calculated to give about l.0-.1.75% of loosely combined sulfur in the mineral oil, such that it is in a condition to provide high cutting efiiciency.
- the quantity of sulfur added is above the range which will enter into simple solution in a light colored pale oil; and the composition is to be distinguished from a simple solution or suspension of sulfur in mineral oil which in concentrations of about 1% or more of sulfur will not withstand storage at low temperatures without sedimentation, even in the presence of stabilizers.
- the temperature and time of heating are critical and are found to lie within the limits of about 300-340 F.
- a material which dissolves in lubricating oil to a clear light colored solution, which possesses extreme pressure properties, and which functions as a stabilizer for the sulfurized mineral oil is added.
- Satisfactory materials of this type are the organic phosphate and phosphite esters, such as tricresyl phosphate, tricresyl phosphite, triphenyl phosphate, triphenyl phosphite, dibutyl phosphate and dibutyl phosphite.
- Suitable extreme pressure bases may be employed, such as halogenated or chlorinated aromatic or aliphatic compounds of the character of chlorinated diphenyl, chlorinated fats and fatty oils, chlorinated wax, and sulfurized diphenyl. Any suitable material known in the art to possess extreme pressure properties and which satisfies the requirements set out above may be employed. Of the materials listed, tricresyl phosphate is preferred from the standpoint of eflectiveness, availability and cheapness of product.
- the extreme pressure base or material is generally added in the proportion of about 13% and preferably about 1-1.5%.
- the extreme pressure material may be added following the sulfurization of the mineral oil and while the same is still at an elevated temperature. Or the extreme pressure material may be first admixed with the mineral oil and then the mixture sulfurized under the conditions set out above.
- a distillate lubricating oil containing about 1.5-3.5% of naturally ccurring sulfur while not possessing high cutting efficiency such as to be suitable for a cutting oil of this type in its naturally produced state, can be sulfurized under substantially similar conditions to those set out above with about 0.8-1.5% of added free sulfur to give a highly effective product having an overall sulfur content of about 2.3-5.0% sulfur, and which is stable against sulfur separation and sedimentation by the use of similar quantitles of the extreme pressure bases set out above. Consequently, where specifications call for a transparent cutting oil of reasonably good color having high sulfur content and which is suitable for high speed cutting operations, such a product is prepared from a high sulfur containing distillate lubricating oil of this character.
- a so-called Sultal viscosity stock which is a dewaxed high sulfur containing distillate lubricating oil of pale color from a naphthene base or Coastal crude, was selected having the following tests:
- a transparent cutting oil of good color conslsting essentially of a pale mineral lubricating oil initially containing about 15-35% of naturally-occurring sulfur and sulfurized by heating with sulfur in the absence of added fatty oil under temperatures of about 300-340" F. and at substantially atmospheric pressure to produce a' loosely combined sulfur content providing an overall sulfur content in excess of about 2.3% and less than about 5.0%, and stabilized with about 1 -3% of an extreme pressure material selected from the group consisting of chlorinated diphenyl, chlorinated fats, chlorinated fatty oils, chlorinat- GUS KAUFMAN.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Lubricants (AREA)
Description
Patented Sept. 15, 1942 CUTTING OIL Gus Kaufman, Beacon, N. Y., assignor, by mesne assignments, to The Texas Company, New York, N. Y., a corporation of Delaware No Drawing. Application March 14, 1939, Serial No. 261,771
1 Claim.
This invention relates to sulfurized lubricants, such as cutting oils, and more particularly to light colored or transparent cutting oils of this character.
Cutting oils as heretofore employed have frequently been composed of fatty or animal oils, and blends of mineral oil with fatty oils. It has also been proposed to sulfurize blends of animal oil and mineral oil, but in such case, the sulfur is taken up ahnost entirely by the more reactive fatty oil to produce a product in which the sulfur is in stable tightly combined form with the fatty oil and diluted by the mineral oil. Cutting oils have also been prepared by incorporating sulfur directly with mineral oil, generally under relatively high temperatures and frequently under superatmospheric pressure to produce a product in which the sulfur is sufiiciently combined with the mineral oil as to resist sulfur separation and sedimentation upon storage.
The earlier cutting oils consisting of simple fatty oils or blends thereof, as well as the sulfurized blends of mineral oil and fatty oil where the sulfur is taken up ahnost entirely by the fatty oil, do not possess the high cutting efficiency demanded by high speed cutting operations of the present time. The' same is true of the straight sulfurized mineral oils where the sulfur is stably and tightly combined with the mineral oil.
In my copending application Serial No. 180,573, filed December 18, 1937, now U. S. Patent No. 2,167,439, dated July 25, 1939, the production of a cutting oil of superior cutting efficiency is described by sulfurizing a straight mineral lubricating oil with uncombined sulfur in the absence of added fatty oil or other highly reactive cn-' stituents which would preferentially combine with the sulfur, at arelatively low and critical temperature range of the order of about 310-360 F. and at atmospheric pressure-to give approximately 2-3% of loosely combined sulfur in the mineral oil, and then stabilizing this sulfurized oil against sulfur separation and sedimentation by the addition of about 2-3% of a fatty oil or a separately sulfurized fatty oil. While such a pi pduct is outstanding in cutting efliciency and is eminently satisfactory for most cutting tool operations, it is comparatively dark in color and does not fall under the classification of a transparent cutting oil.
For some time, the trade has been seeking a light colored transparent cutting oil having high cutting efliciency which is particularly suitable good visibility of the cutting tool and work is required. While there have been scattered products on the market termed transparent cutting oils, these have either been too dark in color to properly fallunder this classification, or else have been lacking in cutting efliciency and unsuitable for high speed operations.
It is an object of the present invention to provide a transparent cutting oil which meets the demand both with respect to color and transparency as well as high cutting efllciency.
I have discovered that a satisfactory transparent cutting oil of this character can be produced by sulfurizing a light colored pale mineral lubricating oil under controlled conditions of comparatively low temperature and at atmospheric pressure so as to provide about 1,0435% loosely combined sulfur in the oil, and then enhancing the cutting efiiciency and at the same time stabilizing th sulfurized oil by the addition of a small proportion of certain oil soluble materials of the character of extreme pressure bases, such as tricresyl phosphate.
In the preparation of my improved product, a mineral lubricating oil or lubricating oil blend, containing light colored pale lubricating oils having a Saybolt Universal viscosity at 100 F. of about 100-l80 seconds, is sulfurized by heating with free sulfur in the absence of added fatty oil or other constituents highly reactive with sulfur at a temperature of about 300-340" F. and preferably about 320 F. for a controlled period of time. The quantity of sulfur employed is calculated to give about l.0-.1.75% of loosely combined sulfur in the mineral oil, such that it is in a condition to provide high cutting efiiciency. The quantity of sulfur added is above the range which will enter into simple solution in a light colored pale oil; and the composition is to be distinguished from a simple solution or suspension of sulfur in mineral oil which in concentrations of about 1% or more of sulfur will not withstand storage at low temperatures without sedimentation, even in the presence of stabilizers. The temperature and time of heating are critical and are found to lie within the limits of about 300-340 F. with a period of heating of from about 1-4 hours at the upper temperature specified, in' order to give-a product of good color with a light colored pale oil in which the sulfur is actually reacted with the mineral lubricating for certain specialized cutting operations where oil in a loosely bound form possessing the required high cutting eihciency, and yet can be stabilized against objectionable sulfur sedimentation upon storage at low temperatures by the addition of small amounts of effective stabilizers of this invention.
To the sulfurized mineral oil prepared as above described, and containing sulfur in a loosely bound form, is added a material which dissolves in lubricating oil to a clear light colored solution, which possesses extreme pressure properties, and which functions as a stabilizer for the sulfurized mineral oil. Satisfactory materials of this type are the organic phosphate and phosphite esters, such as tricresyl phosphate, tricresyl phosphite, triphenyl phosphate, triphenyl phosphite, dibutyl phosphate and dibutyl phosphite. Other suitable extreme pressure bases may be employed, such as halogenated or chlorinated aromatic or aliphatic compounds of the character of chlorinated diphenyl, chlorinated fats and fatty oils, chlorinated wax, and sulfurized diphenyl. Any suitable material known in the art to possess extreme pressure properties and which satisfies the requirements set out above may be employed. Of the materials listed, tricresyl phosphate is preferred from the standpoint of eflectiveness, availability and cheapness of product. The extreme pressure base or material is generally added in the proportion of about 13% and preferably about 1-1.5%. The extreme pressure material may be added following the sulfurization of the mineral oil and while the same is still at an elevated temperature. Or the extreme pressure material may be first admixed with the mineral oil and then the mixture sulfurized under the conditions set out above.
In order to further disclose the invention, the following example is given, it being understood that the example is merely for purposes of illustration and the invention is not restricted thereto:
A blend of 135.6 pounds of 100 E pale oil and 67.8 pounds of 180 C pale oil was used. These oils were light colored paraflin base lubricating distillates having the following tests respectively:
100 E pale 180 C pale oil oil Gravity 28. 8 27. 1 Flash 350 375 Fire 395 435 Viscosity at 100 F., S. U 98 184 Pour F 20 20 Color-Lovibond 95/ 130/6" i temperature. The mix was then allowed to cool gradually for several hours and was drawn off through a 100 mesh screen to remove any suspended solids. The resulting product was a light pale oil having the following tests:
Gravity A. P. I 27.3 Viscosity at 100 F., S. U 119 Color-Lovibond cell 35 Sulfurper cent 1.15 Tricresyl phosphate-per cent 1.0
In a freezing test wherein the product was main tained for 120 hours at 3035 F., it showed a slight wax cloud but no sulfur separation. Cutting tests showed it to be comparable in efficiency to the best cutting oils on the market, including the dark colored products of high sulfur content which are too dark to be classified under transparent cutting oils.
While the combination of the extreme pressure base with the sulfurized mineral oil prepared as set out above gives this superior type of transparent product having high cutting emciency, it is found that the simple addition of these extreme pressure bases to a pale mineral oil of this character, even in substantial proportions, does not produce a cutting il possessing satisfactory cutting efliciency.
As pointed out above, higher percentages of added sulfur than about 1.5% may not as a rule be loosely combined with a pale lubricating oil to produce a light-colored transparent cutting oil which can be stabilized against sulfur separation on storage at low temperatures. However, I have further found that a transparent cutting oil of satisfactory color but containing a higher percentage of overall sulfur content can be produced by sulfurizing a high sulfur containin distillate lubricating oil of pale color. For example, a distillate lubricating oil containing about 1.5-3.5% of naturally ccurring sulfur, while not possessing high cutting efficiency such as to be suitable for a cutting oil of this type in its naturally produced state, can be sulfurized under substantially similar conditions to those set out above with about 0.8-1.5% of added free sulfur to give a highly effective product having an overall sulfur content of about 2.3-5.0% sulfur, and which is stable against sulfur separation and sedimentation by the use of similar quantitles of the extreme pressure bases set out above. Consequently, where specifications call for a transparent cutting oil of reasonably good color having high sulfur content and which is suitable for high speed cutting operations, such a product is prepared from a high sulfur containing distillate lubricating oil of this character. As an example of a cutting oil of this type, the following is given. A so-called Sultal viscosity stock, which is a dewaxed high sulfur containing distillate lubricating oil of pale color from a naphthene base or Coastal crude, was selected having the following tests:
Viscosity at 100 F., S. U Pour, F +15 Coldr-Lovibond 10 Sulfurper cent 2.53
Gravity, A. P. I 23.6 Viscosity at 100 F., S. U 106 Color-Lovibond cell, 25 Sulfur, per cent 3.61 Tricresyl phosphateper cent 1.0
In a freezing test at 30-35 F. for hours,
only a slight cloudiness developed but no sulfur better than the most eflective cutting oils now on the market.
Obviously many modifications and variations of the invention, as hereinbefore set forth, may be made without departing from the spirit and scope thereof, and therefore only such limitations should be imposed as are indicated in the appended claim.
I claim:
A transparent cutting oil of good color conslsting essentially of a pale mineral lubricating oil initially containing about 15-35% of naturally-occurring sulfur and sulfurized by heating with sulfur in the absence of added fatty oil under temperatures of about 300-340" F. and at substantially atmospheric pressure to produce a' loosely combined sulfur content providing an overall sulfur content in excess of about 2.3% and less than about 5.0%, and stabilized with about 1 -3% of an extreme pressure material selected from the group consisting of chlorinated diphenyl, chlorinated fats, chlorinated fatty oils, chlorinat- GUS KAUFMAN.
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2296037A true US2296037A (en) | 1942-09-15 |
Family
ID=3432858
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US2296037D Expired - Lifetime US2296037A (en) | Cutting oil |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2296037A (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2441496A (en) * | 1942-11-09 | 1948-05-11 | Continental Oil Co | Lubricating oils |
| US2467137A (en) * | 1945-12-28 | 1949-04-12 | Standard Oil Dev Co | Metalworking lubricant |
| US2626240A (en) * | 1949-06-25 | 1953-01-20 | Texas Co | Noncorrosive soluble oil containing active sulfur |
| US2655478A (en) * | 1949-06-25 | 1953-10-13 | Texas Co | Noncorrosive soluble oil containing active sulfur |
| US2695877A (en) * | 1950-03-01 | 1954-11-30 | Socony Vacuum Oil Co Inc | Water-in-oil soluble oil |
| US2786031A (en) * | 1951-06-23 | 1957-03-19 | Texas Co | Transparent cutting oil containing active sulfur and sulfochlorinated mono-olefin polymer |
| US3167511A (en) * | 1961-04-13 | 1965-01-26 | Socony Mobil Oil Co Inc | Metal working lubricant |
| US3252908A (en) * | 1963-11-07 | 1966-05-24 | Lubrizol Corp | Lubricating oil and additive composition |
| US4125471A (en) * | 1977-08-03 | 1978-11-14 | Standard Oil Company A Corporation Of Indiana | Sulfurized oil |
| US4228021A (en) * | 1974-12-17 | 1980-10-14 | Exxon Research & Engineering Co. | Chloro-sulphur additive |
-
0
- US US2296037D patent/US2296037A/en not_active Expired - Lifetime
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2441496A (en) * | 1942-11-09 | 1948-05-11 | Continental Oil Co | Lubricating oils |
| US2467137A (en) * | 1945-12-28 | 1949-04-12 | Standard Oil Dev Co | Metalworking lubricant |
| US2626240A (en) * | 1949-06-25 | 1953-01-20 | Texas Co | Noncorrosive soluble oil containing active sulfur |
| US2655478A (en) * | 1949-06-25 | 1953-10-13 | Texas Co | Noncorrosive soluble oil containing active sulfur |
| US2695877A (en) * | 1950-03-01 | 1954-11-30 | Socony Vacuum Oil Co Inc | Water-in-oil soluble oil |
| US2786031A (en) * | 1951-06-23 | 1957-03-19 | Texas Co | Transparent cutting oil containing active sulfur and sulfochlorinated mono-olefin polymer |
| US3167511A (en) * | 1961-04-13 | 1965-01-26 | Socony Mobil Oil Co Inc | Metal working lubricant |
| US3252908A (en) * | 1963-11-07 | 1966-05-24 | Lubrizol Corp | Lubricating oil and additive composition |
| US4228021A (en) * | 1974-12-17 | 1980-10-14 | Exxon Research & Engineering Co. | Chloro-sulphur additive |
| US4125471A (en) * | 1977-08-03 | 1978-11-14 | Standard Oil Company A Corporation Of Indiana | Sulfurized oil |
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